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Commercialisation of acidic geothermal wells by ph buffering

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As. J. Energy Env. 2005, 6(03), 175-185 178The HCO3 - has an equilibrium pH <strong>of</strong> 8-10. This method had been overlooked from atheoretical standpoint. It is true that the injection <strong>of</strong> CO2 or the re-injection <strong>of</strong> NCG adjuststhe ge<strong>of</strong>luid to a more stable non-corrosive pH <strong>of</strong> 8.35. However, when the ge<strong>of</strong>luid isallowed to flow out <strong>of</strong> the well, the pressure drops, and the temperature remains high,resulting in a substantial decrease in the solubility <strong>of</strong> CO2. As the concentration <strong>of</strong> dissolvedCO2 drops, the natural <strong>buffering</strong> effect <strong>of</strong> CO2 is affected; as a result, the natural acidity<strong>of</strong> the ge<strong>of</strong>luid makes this technique futile for adjusting the pH. This method had been triedin the Philippines but was eventually rejected.The technique <strong>of</strong>commercializing <strong>acidic</strong> <strong>wells</strong> through the use <strong>of</strong> acid resistant materials<strong>of</strong> construction for the steam gathering system and well casing would entail high initialfixed cost that is not feasible in third world countries, like the Philippines. This wouldlikewise result in a high cost <strong>of</strong> power conversion <strong>of</strong> <strong>geothermal</strong> energy making it lessfavorable compared to other sources <strong>of</strong> energy.Materials and MethodologiesBuffer and Buffer CapacityA buffer, composed <strong>of</strong> a weak acid and its strong salt with a strong base or a weak base andits strong salt with a weak acid, has the ability to maintain the pH <strong>of</strong> a solution betweennarrow limits [11]. Therefore, a buffered solution will have no appreciable change in its pHupon dilution or addition <strong>of</strong> slight to moderate amounts <strong>of</strong> a strong acid or base. Buffercapacity is a measure <strong>of</strong> the ability <strong>of</strong> the buffer system to neutralize added strong acid orbase without a significant change in pH. The resistance to change in pH <strong>of</strong> a solution isgreatest when [acid] / [salt] =1.Therefore, buffer capacity is a maximum for buffer solutionscontaining equivalent amounts <strong>of</strong> a weak acid and its salt.As the ratio [acid]/[salt] changesfrom unity,either <strong>by</strong> decreasing or increasing the acid concentration or the salt concentration,the buffer capacity changes.A solution is generally considered to have a useful buffercapacity if the[acid] to [salt] ratio is within the range from 0.1 to 10;hence, effective withinthe range pK a ± 1 [11].New Buffering SolutionThe new buffer used in this investigation is ß - chloropropionic acid- sodium - ß-chloropropionate (BCPH- NaBCP) with a pKa = 4.11 [10] and a boiling point <strong>of</strong> 205 o C[7]. It has a high decomposition point in water (>200) via hydrolysis (Merck Index, 1989).This buffer system was chosen because the designed pH is within 4.11 ± 1 which is theeffective buffer range [11] and will not react with ge<strong>of</strong>luid components.For more than three years now, an extensive study <strong>of</strong> applying pH <strong>buffering</strong> to solvecorrosion and silica-scaling problems encountered in <strong>geothermal</strong> systems [21] has beenconducted.Cabigon had successfully tested this method in the laboratory for silicadissolution without affecting low carbon steel casing.

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